Porous acidic resin catalyst, preparation method and applications thereof

A technology of acidic resin and catalyst, which is applied in the field of catalyst preparation, can solve the problems of low reactivity, small amount of acid on the pore surface, limited reaction diffusion, etc. Large volume and specific surface area, good reaction diffusivity

Inactive Publication Date: 2016-06-01
JIANGSU HELPER FUNCTIONAL MATERIALS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] CN101544562A has invented a method for zeolite molecular sieve to catalyze acetic acid and butene to synthesize sec-butyl acetate, using butene and acetic acid as raw materials, using modified beta zeolite molecular sieve as catalyst, and continuously synthesizing sec-butyl acetate in a fixed-bed reactor; However, the zeolite molecular sieve catalyst is easy to form carbon at the reaction temperature of 90-130°C, and the reaction deactivation is relatively fast. Therefore, although it does not have the strong corrosiveness and toxicity of sulfuric acid, the catalyst has the problem of poor long-term use stability, which restricts its industrial application
However, the ordinary styrene-divinylbenzene cation exchange resin itself has small pore volume and specific surface area, and a small amount of acid on the pore surface, which causes the problem that its reaction diffusion as a solid acid catalyst is limited, so that it is used in heterogeneous catalysis. Low reactivity and selectivity in application
Chinese patent CN101948385A has proposed a kind of synthetic method of sec-butyl acetate, and the used catalyst of reaction is macroporous strongly acidic cation exchange resin; Because common macroporous strongly acidic cation exchange resin specifi

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0035] (1) nanomaterial modification: the nano CaCO with 70 parts by weight and a particle size of 10nm 3 The material powder and 30 parts of propionic acid were reacted in 50 parts of acetone solvent at 50°C for 3 hours; then evaporated at 100°C to remove the acetone solvent, and the mesoporous nano-CaCO 3 The surface of the material is esterified and modified to obtain a hydrophobic modified porous nanometer material.

[0036] (2) Polymer suspension polymerization synthesis: 40wt% styrene monomer, 10wt% dipenylbenzene copolymerized crosslinking monomer, 3wt% azobisisobutyronitrile initiator, 3wt% modified nano-CaCO 3 Material, 15% toluene porogen and 29wt% petroleum ether solvent are made into oil phase solution A;

[0037] Pure water, gum arabic dispersant and titanium oxide dispersant are formulated as aqueous phase solution B, and the weight ratio of pure water, gum arabic dispersant and titanium oxide dispersant is 100:1.6:1.4, oil phase solution A and aqueous phase sol...

Embodiment 2

[0041] (1) Modification of porous nanomaterials: 95 parts by weight and a particle size of 200nm nano-CaCO 3 The material and 5 parts of propionic acid were reacted in 40 parts of acetone solvent at 60°C for 1 hour; then evaporated at 80°C to remove the acetone solvent, and the inorganic nano-CaCO 3 Hydrophobic modification of material carrier.

[0042] (2) Synthesis of resin polymerization: 60wt% butylene monomer, 2wt% divinylbenzene copolymerized crosslinking monomer, 0.1wt% dicumyl peroxide initiator, 20wt% modified nano-CaCO 3 Material, 5% butanol porogen and 12.9wt% n-hexane solvent are made into oil phase solution A;

[0043] With pure water, gum arabic dispersant and titanium oxide dispersant as aqueous phase solution B, the weight ratio of pure water, gum arabic dispersant and titanium oxide dispersant is 100:2.0:1.5, oil phase solution A and aqueous phase solution B Mix at a weight ratio of 1:2.5, heat up to 83°C for 3 hours under stirring at 240 rpm, cool down, fil...

Embodiment 3

[0048] (1) Nanomaterial modification: 80 parts by weight and a particle size of 100nm nano-Al 2 o 3 The material and 20 parts of propionic acid were reacted in 45 parts of acetone solvent at 55 ° C for 2 hours; then evaporated at 90 ° C to remove the acetone solvent, that is, to complete the inorganic nano-Al 2 o 3 Hydrophobic modification of material carrier.

[0049] (2) Polymer resin suspension polymerization: 30wt% methyl methacrylate monomer, 15wt% divinyl phenyl methyl copolymer crosslinking monomer, 1.0wt% dicumyl peroxide initiator, 10wt% modified Nano-Al 2 o 3 Material, 15% n-heptane porogen and 29wt% butanone solvent are made into oil phase solution A;

[0050] Using pure water, gelatin dispersant and titanium oxide dispersant as aqueous phase solution B, the weight ratio of pure water, gelatin dispersant and titanium oxide dispersant is 100:2:1.5, and the oil phase solution and aqueous phase solution are mixed in a weight ratio of 1 : 2.8 mixed, heated up to 8...

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Abstract

The present invention provides a porous acidic resin catalyst, wherein a nanometer material adopted as a pore forming hard template agent is directly doped into a macromolecule resin, reaction dissolving is performed in an acid solution to remove the nanometer material so as to form nanometer pore channels in the macromolecule resin, and then a sulfonation reaction is performed to achieve acid functionalization so as to prepare the nano-pore resin solid acid. The present invention further provides a preparation method and applications of the porous acidic resin catalyst. According to the present invention, the porous acidic resin catalyst has characteristics of large pore volume, large specific surface area, and strong acidity; and with the application of the porous acidic resin catalyst as the solid acid catalyst in the catalytic reaction for esterification synthesis of sec-butyl acetate from acetic acid and butene, the reaction activity is high, the reaction stability is good, and the butene conversion rate and the sec-butyl acetate yield of the esterification reaction can be significantly improved.

Description

technical field [0001] The invention belongs to the field of catalyst preparation, in particular to a porous acidic resin catalyst used for esterifying acetic acid and butene to synthesize sec-butyl acetate. Background technique [0002] Acetate is catalyzed direct addition and esterification of propylene, 1-butene, 2-butene, isobutene and other lower alkenes with acetic acid or other carboxylic acids to produce corresponding isopropyl acetate, sec-butyl acetate and isobutyl acetate Esters and other acetates and other carboxylates. At present, the products with the broadest market prospects are isopropyl acetate and sec-butyl acetate. [0003] Secondary butyl acetate, also known as additional butyl acetate, second butyl acetate, is one of the four isomers of butyl acetate, a colorless, flammable, fruity liquid, and other isomers Performance is similar in most cases and can dissolve a wide variety of resins and organics. Its boiling point is lower than that of commonly use...

Claims

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Application Information

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IPC IPC(8): B01J31/10C07C69/14C07C67/04
Inventor 朱志荣蔡建国李晓红石洪雁
Owner JIANGSU HELPER FUNCTIONAL MATERIALS
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